Microwave Regenerable GAC with Oxidation by Microwaves and Catalyst—(CHA Corp.)

 

Description of Technology

The CHA Corporation's technology removes solvents from gas streams by adsorption onto GAC with regeneration of the saturated carbon by microwave energy.  After desorption, the solvents or VOCs are carried by a nitrogen purge gas stream to a destruction chamber where microwaves induce oxidation reactions on the surface of a palladium catalyst.  In addition to removing and destroying VOCs from waste streams, the technology also removes sulfur dioxide (SO2) and oxides of nitrogen (NOx). A zeolite bed can also be added to remove ammonia and acid gases that are not easily adsorbed onto GAC.  One system designed by the CHA Corporation involves a transfer of the contaminated carbon to a separate regenerator for desorption of the contaminants while another system has an “all-in-one” adsorption and regeneration system.

 

Figure 1 below shows a diagram of the microwave air purification system with all-in-one adsorption/regeneration and oxidation system.

 

 

As the diagram illustrates, the system has four main components, a moving-bed GAC/zeolite adsorber, microwave regenerator, microwave oxidizer, and acid gas adsorber.  The moving-bed adsorber continuously treats the air stream containing VOCs, hydrocarbons, solvents and acid gases by adsorption of these contaminants onto the 4-inch thick moving bed of 3-mm, 80 carbon tetrachloride number pelletized GAC, while the 2-inch thick, 4 X 8-mesh natural zeolite bed removes any acid gases and ammonia. 

 

The concentrated stream produced by the regeneration of the saturated GAC by microwave energy, approximately 1% of the volume of the original air stream, is then cooled and condensed to a liquid.  This liquid solvent is collected in a knockout pot (not shown), while any remaining solvent vapor in the N2 sweep gas from the GAC regenerator is fed into the microwave based catalytic oxidizer.  The microwave catalyst reactor is packed with an oxidizing catalyst of platinum (Pt) and palladium (Pd) coated onto alumina beads impregnated with 25 percent 800-mesh SiC.  The contaminant stream with solvents and gases in the N2 is mixed with sufficient air for combustion and fed to the oxidizer.  The microwaves and catalyst work together to oxidize the concentrated solvent/acid gas-laden stream at low temperatures.  The regenerated GAC and zeolite are then returned to the top of the adsorber.  The combustion products from chlorinated solvents will be CO2, H2O and HCl, which flows through an acid gas scrubber.  The scrubber is a caustic impregnated carbon bed.  Clean air from the gas exiting the acid-gas removal bed is mixed with clean air from the carbon/zeolite adsorber and vented to the atmosphere.

 

Figure 2 shows a picture of the CHA vapor regeneration unit demonstrated at Edwards Air Force Base.  This unit is 1/10th of the size of a full-scale system.

 
Vapor regeneration unitVapor regeneration unit

Vapor regeneration unitVapor regeneration unit

 

 

The CHA technology allows the option of either recovering or destroying solvents, ammonia, acids and other air pollutants and the continuous regeneration of the GAC and zeolite on site.  The company claims that no secondary pollutants such as NOx are produced during regeneration and the volume of gas production from the regeneration is 1% of the volume of the contaminated air being treated.  Therefore there is a 100 to 1 reduction in oxidation equipment scale.  The company also claims that the microwave catalytic oxidation of solvents, ammonia and acids eliminates any need for handling and disposal of recovered wastes.  Additionally, less energy is required in the regeneration process than in conventional GAC regeneration since the temperatures are lower.

Vendor

CHA Corporation

372 West Lyon Street

Laramie, WY 82072